EP1839492B1 - Micelles de lactosérum - Google Patents

Micelles de lactosérum Download PDF

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Publication number
EP1839492B1
EP1839492B1 EP06006295A EP06006295A EP1839492B1 EP 1839492 B1 EP1839492 B1 EP 1839492B1 EP 06006295 A EP06006295 A EP 06006295A EP 06006295 A EP06006295 A EP 06006295A EP 1839492 B1 EP1839492 B1 EP 1839492B1
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EP
European Patent Office
Prior art keywords
whey protein
micelles
protein
whey
powder
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Not-in-force
Application number
EP06006295A
Other languages
German (de)
English (en)
Other versions
EP1839492A1 (fr
Inventor
Christophe J.E. Schmitt
Lionel Bovetto
Frédéric ROBIN
Matthieu Pouzot
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nestec SA
Original Assignee
Nestec SA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to PL06006295T priority Critical patent/PL1839492T3/pl
Application filed by Nestec SA filed Critical Nestec SA
Priority to EP06006295A priority patent/EP1839492B1/fr
Priority to AT06006295T priority patent/ATE524073T1/de
Priority to ES06006295T priority patent/ES2373400T3/es
Priority to MYPI20070461A priority patent/MY161874A/en
Priority to UAA200812529A priority patent/UA98934C2/uk
Priority to AU2007231336A priority patent/AU2007231336B2/en
Priority to RU2008142397/10A priority patent/RU2417622C2/ru
Priority to CA2643651A priority patent/CA2643651C/fr
Priority to NZ571141A priority patent/NZ571141A/en
Priority to PCT/EP2007/052877 priority patent/WO2007110411A2/fr
Priority to EP07727350A priority patent/EP2001306A2/fr
Priority to CN2007800113474A priority patent/CN101410025B/zh
Priority to US12/280,244 priority patent/US8399043B2/en
Priority to CA2640684A priority patent/CA2640684C/fr
Priority to MX2008012184A priority patent/MX2008012184A/es
Priority to AU2007231346A priority patent/AU2007231346A1/en
Priority to PCT/EP2007/052900 priority patent/WO2007110421A2/fr
Priority to RU2008142396/13A priority patent/RU2008142396A/ru
Priority to UAA200812429A priority patent/UA98763C2/ru
Priority to EP07727373A priority patent/EP1998626A2/fr
Priority to ARP070101277A priority patent/AR060163A1/es
Priority to CN2007800110423A priority patent/CN101410020B/zh
Priority to JP2009502066A priority patent/JP2009531043A/ja
Publication of EP1839492A1 publication Critical patent/EP1839492A1/fr
Priority to IL193863A priority patent/IL193863A/en
Priority to ZA2008/09154A priority patent/ZA200809154B/en
Application granted granted Critical
Publication of EP1839492B1 publication Critical patent/EP1839492B1/fr
Priority to US13/780,975 priority patent/US20130171318A1/en
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

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    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J1/00—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
    • A23J1/20—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from milk, e.g. casein; from whey
    • A23J1/205—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from milk, e.g. casein; from whey from whey, e.g. lactalbumine
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C11/00—Milk substitutes, e.g. coffee whitener compositions
    • A23C11/02—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins
    • A23C11/04—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing non-milk fats but no non-milk proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C21/00—Whey; Whey preparations
    • A23C21/02—Whey; Whey preparations containing, or treated with, microorganisms or enzymes
    • A23C21/026—Whey; Whey preparations containing, or treated with, microorganisms or enzymes containing, or treated only with, lactic acid producing bacteria, bifidobacteria or propionic acid bacteria
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C21/00—Whey; Whey preparations
    • A23C21/08—Whey; Whey preparations containing other organic additives, e.g. vegetable or animal products
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
    • A23G1/00—Cocoa; Cocoa products, e.g. chocolate; Substitutes therefor
    • A23G1/30—Cocoa products, e.g. chocolate; Substitutes therefor
    • A23G1/32—Cocoa products, e.g. chocolate; Substitutes therefor characterised by the composition containing organic or inorganic compounds
    • A23G1/44—Cocoa products, e.g. chocolate; Substitutes therefor characterised by the composition containing organic or inorganic compounds containing peptides or proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
    • A23G1/00—Cocoa; Cocoa products, e.g. chocolate; Substitutes therefor
    • A23G1/30—Cocoa products, e.g. chocolate; Substitutes therefor
    • A23G1/32—Cocoa products, e.g. chocolate; Substitutes therefor characterised by the composition containing organic or inorganic compounds
    • A23G1/46—Cocoa products, e.g. chocolate; Substitutes therefor characterised by the composition containing organic or inorganic compounds containing dairy products
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
    • A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
    • A23G9/32—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by the composition containing organic or inorganic compounds
    • A23G9/38—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by the composition containing organic or inorganic compounds containing peptides or proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
    • A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
    • A23G9/32—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by the composition containing organic or inorganic compounds
    • A23G9/40—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by the composition containing organic or inorganic compounds characterised by the dairy products used
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J3/00—Working-up of proteins for foodstuffs
    • A23J3/04—Animal proteins
    • A23J3/08—Dairy proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L23/00—Soups; Sauces; Preparation or treatment thereof
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
    • A23L27/70—Fixation, conservation, or encapsulation of flavouring agents
    • A23L27/72—Encapsulation
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/17—Amino acids, peptides or proteins
    • A23L33/19—Dairy proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/30—Encapsulation of particles, e.g. foodstuff additives
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/40—Shaping or working of foodstuffs characterised by the products free-flowing powder or instant powder, i.e. powder which is reconstituted rapidly when liquid is added
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C2210/00—Physical treatment of dairy products
    • A23C2210/30—Whipping, foaming, frothing or aerating dairy products
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2200/00—Function of food ingredients
    • A23V2200/20—Ingredients acting on or related to the structure
    • A23V2200/25—Nanoparticles, nanostructures
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
    • Y10T428/2984—Microcapsule with fluid core [includes liposome]

Definitions

  • the present invention relates to whey protein micelles, particularly to whey protein micelle concentrates and powders thereof and to a method for producing them.
  • the present invention also pertains to the use of these micelles concentrates and powders thereof in a wide range of applications.
  • Protein constitutes an indispensable part of the diets of many people. It is not only used for its nutritional value but also imparts desirable texture and stabilisation to foods. For instance, in fat-containing products, the fat must remain stabilized over the entire shelf life of the product, so that no phase separation occurs.
  • emulsifying agents are utilized, that provide a stabilization of the emulsion once formed, based on their inherent property of a lipophilic or hydrophobic part being soluble in the non-aqueous phase and a polar or hydrophilic part being soluble in water such that said molecules facilitate emulsifying one phase in the other phase. Additionally, the emulsifying agents also protect the once formed droplets from aggregation and coalescence. As emulsifying agents naturally occurring substances are used, such as hydrocolloids, phospholipids (lecithin) or glycolipids and on the other hand synthetic agents like stearyl-2-lactylate or mono-, diacylglycerides, etc. may also be used.
  • agents One of the major drawbacks of the agents resides in that they sometimes substantially add to the costs of the final product, and do not add to the nutritional value of the product. Sometimes, such kinds of materials also do not show adequate stabilising properties because of an interfacial competition with proteins.
  • protein is also being used as an emulsifier and as a partial substitute for fat.
  • US 6767575 B1 discloses a preparation of an aggregate whey protein product, whereby whey protein is denatured by acidification and heating. The protein aggregates thus obtained are used in food application.
  • GB 1079604 describes improvements in the manufacture of cheese, whereby whey proteins undergo heat treatment at an optimum pH value, in order to obtain insoluble whey proteins which are then added to raw milk.
  • WO 93/07761 is concerned with the provision of a dry microparticulated protein product which can be used as a fat substitute.
  • US 5750183 discloses a process for producing proteinaceous microparticles which are useful as fat substitute containing no fat.
  • a proteinaceous fat substitute is also disclosed in WO 91/17665 whereby the proteins are in the form of a water-dispersible microparticulated denatured whey protein.
  • proteins are also present in many pharmaceutical and cosmetic compositions.
  • This gel effect presents limitation in terms of not only processability (e.g. clogging of machines used in the manufacture of protein-containing products) but also in terms of the texture thus obtained, which may not be desirable for the wide range of protein applications.
  • Controlled denaturation of proteins is thus desirable in order to widen the use of proteins.
  • EP 0603981 also describes a heat stable oil-in-water emulsion containing proteins.
  • an object of the invention is to improve the usability of proteins in industrial production processes.
  • Whey protein micelles and consumable products comprising said micelles are also disclosed.
  • Figure 7 is a schematic representation of the micelles obtainable by the process of the present invention, wherein the whey proteins are arranged in such a way that the hydrophilic parts of the proteins are oriented towards the outer part of the agglomerate and the hydrophobic parts of the proteins are oriented towards the inner "core" of the micelle.
  • This energetically favourable configuration offers good stability to these structures in a hydrophilic environment.
  • the specific micelle structure can be seen from the figures, in particular figures 3 , 9 , 10 , 13 and 15 , wherein the micelles of the present invention consist essentially of spherical agglomerates of denatured whey protein.
  • hydrophobic phase e.g. a fat droplet or air
  • hydrophilic phase e.g. a hydrophilic phase
  • the micelles produced by the method of the present invention have an extremely sharp size distribution (see Fig. 14 ), such that more than 80% of the micelles produced will have a size smaller than 1 micron, preferably between 100nm and 900nm, more preferably between 100-770nm, most preferably between 200 and 400nm.
  • the mean diameter of the micelles can be determined using Transmission Electron Microscopy (TEM).
  • TEM Transmission Electron Microscopy
  • the liquid micelle samples are encapsulated in agar gel tubes. Fixation is achieved by immersion in a solution of 2.5% glutaraldehyde in 0.1M, pH 7.4 cacodylate buffer and post-fixation with 2% Osmium tetroxide in the same buffer, both solutions containing 0.04% Ruthenium red. After dehydration in a graded ethanol series (70, 80, 90, 96, 100% ethanol), the samples are embedded in Spurr resin (Spurr/ethanol 1:1, 2:1, 100%).
  • the micelles described above are produced by a process according to the present invention, said process being described in detail in the following.
  • any commercially available whey protein isolates or concentrates may be used, i.e. whey protein obtained by any process for the preparation of whey protein known in the art, as well as whey protein fractions prepared therefrom or proteins such as ⁇ -lactoglobulin (BLG), ⁇ -lactalbumin and serum albumin.
  • whey protein obtained by any process for the preparation of whey protein known in the art, as well as whey protein fractions prepared therefrom or proteins such as ⁇ -lactoglobulin (BLG), ⁇ -lactalbumin and serum albumin.
  • sweet whey obtained as a by-product in cheese manufacture acid whey obtained as a by-product in acid casein manufacture
  • native whey obtained by milk microfiltration or rennet whey obtained as a by-product in rennet casein manufacture may be used as the whey protein.
  • the whey protein may be from a single source or from mixtures of any sources.
  • the present invention is not restricted to whey isolates from bovine origin, but pertains to whey isolates from all mammalian animal species, such as from sheep, goats, horses, and camels.
  • the process according to the present invention applies to demineralised whey preparations.
  • Whey proteins are an excellent source of essential amino acids (AA) (45%). Compared to casein (containing 0.3g cysteine/100g protein), sweet whey proteins contain 7 times more cysteine, and acid whey 10 times more cysteine. Cysteine is the rate limiting amino acid for glutathione (GSH) synthesis, a tripeptide made of glutamate cysteine and glycine which has primary important functions in the defence of the body in case of stress. Requirements in these amino acids may be increased in case of stress and in elderly people. Also, glutathione oral supplementation with whey protein has been shown to increase plasma GSH levels of HIV-infected patients ( Eur. J. Clin. Invest. 2001; 31, 171-178 ).
  • whey proteins include enhancement of muscle development and building, as well as muscle maintenance in children, adults or elderly people, enhancement of the immune function, improvement of cognitive function, control of blood glucose such that they are suitable for diabetics, weight management and satiety, anti-inflammatory effects, wound healing and skin repair, lowering of the blood pressure, etc.
  • whey proteins may be present in an aqueous solution in an amount of less than 12%, preferably of 0.1 wt.% to less than 12 wt.%, preferably in an amount of 0.1 wt.% to 8 wt.%, more preferably in an amount of 0.2 wt.% to 7 wt.%, even more preferably in an amount of 0.5 wt.% to 6 wt.%, most preferably in an amount of 1 wt.% to 4 wt.% on the basis of the total weight of the solution.
  • the aqueous solution of the whey protein preparation as present before the micellisation step may also comprise additional compounds, such as by-products of the respective whey production processes, other proteins, gums or carbohydrates.
  • the solution may also contain other food ingredients (fat, carbohydrates, plant extracts, etc). The amount of such additional compounds does not exceed 10 wt.% of the total weight of the solution.
  • the whey protein, as well as the fractions and/or the main proteins thereof may be used in purified form.
  • the content of divalent cations in the whey protein for the preparation of the whey protein micelles concentrate may be less than 2.5%, more preferably less than 2%, even more preferably less than 0.2%.
  • Most preferably the whey proteins are completely demineralised.
  • the pH and the ionic strength are important factors in the present method.
  • free cations such as Ca, K, Na, Mg
  • These micelles will have an overall negative charge.
  • the same micelle form can also be obtained symmetrically below the isoelectrical pH, i.e from 3.5 to 5.0, more preferably 3.8 to 4.5, resulting in micelles being positively charged (see Figure 6 ).
  • micellisation of whey proteins may be done in a salt free solution at a pH value adjusted between 3.8 and 4.5 depending on the mineral content of the protein source.
  • the micelles obtained will have an overall negative charge.
  • the pH is adjusted to a range of from 6.3 to 9.0, for a content in divalent cations comprised between 0.2% and 2.5% in whey protein powder.
  • the pH is adjusted to a range of from 5.6 to 6.4, more preferably from 5.8 to 6.0 for a low divalent cation content (e.g. less than 0.2% of the initial whey protein powder).
  • the pH may be increased up to 8.4 depending on the mineral content of whey protein source (concentrate or isolate).
  • the pH may be between 7.5 to 8.4, preferably 7.6 to 8.0 to obtain negatively charged micelles in the presence of large amounts of free minerals and the pH may be between 6.4 to 7.4, preferably 6.6 to 7.2 to obtain negatively charged micelles in the presence of moderate amounts of free minerals.
  • the higher the calcium and/or magnesium content of the initial whey protein powder the higher the pH of micellisation.
  • the present invention it is required to demineralise by any of the known demineralisation techniques (dialysis, ultrafiltration, reverse osmosis, ion exchange chromatography%), any source of liquid native whey proteins with a protein concentration ranging from that of sweet whey, microfiltration permeate of milk or acid whey (0.9% protein content) to that of a concentrate at 30% protein content.
  • the dialysis can be done against water (distilled, deionised or soft), but as this will only allow removal of the ions weakly bound to the whey proteins, it is more preferable to dialyse against an acid at pH below 4.0 (organic or inorganic) to better control the ionic composition of the whey proteins.
  • the pH of whey protein micelle formation will be comprised between 5.8 to 6.6.
  • the pH Prior to heating the whey protein aqueous solution, the pH is generally adjusted by the addition of acid, which is preferably food grade, such as e.g. hydrochloric acid, phosphoric acid, acetic acid, citric acid, gluconic acid or lactic acid.
  • acid which is preferably food grade, such as e.g. hydrochloric acid, phosphoric acid, acetic acid, citric acid, gluconic acid or lactic acid.
  • alkaline solution which is preferably food grade, such as sodium hydroxide, potassium hydroxide or ammonium hydroxide.
  • ionic strength may be adjusted by organic or inorganic ions in such a way that allows micellisation at a constant pH value of 7.
  • Figure 4 represents an embodiment of the present invention, whereby micelles may be formed at a constant pH value of 7.0 while the ionic strength is varied by the addition of 70-80 mM of arginine HCl.
  • a buffer may be further added to the aqueous solution of whey protein so as to avoid a substantial change of the pH value during heat treatment of the whey protein.
  • the buffer may be selected from any food-grade buffer system, i.e. acetic acid and its salts, such as e.g. sodium acetate or potassium acetate, phosphoric acid and salts thereof, e.g. NaH 2 PO 4 , Na 2 HPO 4 , KH 2 PO 4 , K 2 HPO 4 , or citric acid and salts thereof etc.
  • Adjusting the pH and the ionic strength of the aqueous solution, according to the present invention results in a controlled process yielding micelles having a size between 100nm-900nm, preferably between 100-700nm, most preferably between 200-400nm.
  • the proportion of micelles with an average size comprised between 100-700nm is greater than 80% when carrying out the process of the invention (see Figure 14 ).
  • the starting whey protein aqueous solution is then subjected to the heat treatment.
  • the temperature in the range of from 80 to 89 °C, more preferably of from 84 to 87 °C, most preferred at about 85 °C.
  • the desired temperature is kept at this temperature for a minimum of 10 seconds and a maximum of 2 hours.
  • the time period during which the aqueous whey protein solution is kept at the desired temperature ranges from 12 to 25 minutes, more preferably from 12 to 20 minutes, or most preferably about 15 minutes.
  • the heat treatment may also be achieved in a microwave oven or any similar equipment allowing heating by microwaves with a time/quantity ratio of 10 s/10 mL for a 4 wt% protein solution heated in a 1500 W apparatus up to boiling temperature (98°C at an altitude of 833m).
  • a continuous process may also be used by addition of 8 or more magnetrons around a glass tube potentially prolonged by a holding tube to increase the time of incubation.
  • turbidity measurements are an indication of micelle formation.
  • the turbidity measured by absorbance at 500nm is at least 3 absorbance units for 1% protein solution but can reach 16 absorbance units when the yield of micellisation is above 80% (see Figure 2 ).
  • Table 1 Physicochemical properties of soluble whey protein aggregates obtained by heat treatment (85°C, 15 min) of a 1 wt% protein dispersion in presence or absence of NaCl. pH hydrodynamic diameter (nm) molecular weight M w (x 10 6 g.mol -1 ) morphology ⁇ -potential (mV) protein surface hydrophobicity ( ⁇ g.mmol - 1 ANS) accessible SH groups (nmol SH.mg -1 prot.) 6.0 120.3 ⁇ 9.1 27.02 ⁇ 8.09 Spherical micelles -31.8 ⁇ 0.8 105.4 3.5 ⁇ 0.4 6.8 56.2 ⁇ 4.6 0.64 ⁇ 0.01 linear aggregates -27.9 ⁇ 1.2 200.8 6.8 ⁇ 0.5
  • the conversion yield of native whey protein to micelles decreases when the initial protein concentration is increased before pH adjustment and heat treatment.
  • the yield of formation of whey protein micelles drops from 85% (when starting with 4% proteins) to 50% (when starting with 12% of proteins).
  • the protein concentration is adjusted before heat treatment to manage the optimal whey protein micelles yield.
  • the whey proteins micelles obtained according to the present method shall have an average size of less than 1 ⁇ m, preferably of from 100 to 900 nm, more preferably from 100 to 700 nm, most preferably from 200-400nm.
  • the yield of micelles before concentration is at least 35%, preferably at least 50%, more preferably at least 80% and the residual soluble aggregates or soluble protein content is preferably below 20%.
  • the average micelle size is characterised by a polydispersity index below 0.200.
  • An advantage of the method of the present invention is that the whey protein micelles prepared accordingly have not been submitted to any mechanical stress leading to reduction of the particle size during formation, contrary to conventional processes. This method induces spontaneous micellisation of whey proteins during heat treatment in the absence of shearing.
  • the whey protein micelles may be used as such in any composition, such as nutritional compositions, cosmetic compositions, pharmaceutical compositions etc.
  • the whey protein micelles may be filled with an active component.
  • Said component may be selected from coffee, caffeine, green tea extracts, plant extracts, vitamins, minerals, bioactive agents, salt, sugar, sweeteners, aroma, fatty acids, oils etc. and mixtures thereof.
  • the whey protein micelles (pure or filled with active components) may be coated with an emulsifier such as phospholipids, for example, or other coating agents such as acacia gum in order to modulate the functionality and the taste of the whey protein micelles.
  • the coating is an emulsifier selected from sulphated butyl oleate, diacetyltartaric acid esters of mono- and diglycerides, citric acid esters of monoglycerides, stearoyl lactylates and mixtures thereof.
  • Fig. 17 is a schematic representation of such coating with sulphated butyl oleate.
  • the whey protein micelles have shown to be ideally suited for use as an emulsifier, fat substitute, substitute for micellar casein or foaming agent, since they are able to stabilize fat and/or air in an aqueous system for prolonged period.
  • whey protein micelles may be used as an emulsifying agent, for which the material is ideally suited, since it has a neutral taste and no off-flavour is created by the use of such material. They may also be used as micellar casein substitute.
  • the present whey protein micelles are still in a condition to serve as whitening agent, so that with one compound several tasks may be fulfilled. Since whey is a material abundantly available, the use thereof reduces the cost of a product requiring an emulsifying, filling, whitening or foaming agent, while at the same time adding to its nutritional value.
  • the whey protein micelles obtained according to the method of the present invention can be used for the preparation of any kind of consumable product requiring stabilisation of an emulsion or a foam, such as e.g. present in mousse or ice cream, in coffee creamers, or also in low fat or essentially fat free dairy products, or also where it finds application as a micellar casein substitute.
  • consumable is meant any food product in any form, including beverages, soups, semi-solid foods etc. which can be consumed by a human or an animal.
  • Examples for products, where the present whey protein micelles may find application are for example, dairy products, mayonnaise, salad dressing, pasteurized UHT milk, sweet condensed milk, yoghurt, fermented milks, sauces, reduced fat sauces such as béchamel sauce for instance, milk-based fermented products, milk chocolate, white chocolate, dark chocolate, mousses, foams, emulsions, ice creams, fermented cereal based products, milk based powders, infant formula, diet fortifications, pet food, tablets, liquid bacterial suspensions, dried oral supplement, wet oral supplement, performance nutrition bars, spreads, fruit drinks, coffee mixes.
  • dairy products mayonnaise, salad dressing, pasteurized UHT milk, sweet condensed milk, yoghurt, fermented milks, sauces, reduced fat sauces such as béchamel sauce for instance, milk-based fermented products, milk chocolate, white chocolate, dark chocolate, mousses, foams, emulsions, ice creams, fermented cereal
  • the present whey protein micelles may be used either alone or together with other active materials, such as polysaccharides (e.g. acacia gum or carrageenans) to stabilize matrices and for example milky foam matrices. Due to their neutral taste, their whitening power and their stability after heat treatment, the present whey proteins micelles may be used to increase skimmed milk whiteness and mouth feel.
  • active materials such as polysaccharides (e.g. acacia gum or carrageenans) to stabilize matrices and for example milky foam matrices. Due to their neutral taste, their whitening power and their stability after heat treatment, the present whey proteins micelles may be used to increase skimmed milk whiteness and mouth feel.
  • the fat content in a food matrix may be reduced.
  • This feature represents a particular advantage of the present whey protein micelles, since it allows producing low-fat products, for example adding a milk creamer without adding additional fat derived from the milk as such.
  • the whey protein micelle dispersion obtained after heat treatment is concentrated to yield a whey protein micelle concentrate.
  • the concentration step may be carried out by evaporation, centrifugation, sedimentation and/or by microfiltration.
  • Evaporation may be carried out on the micelles dispersion by feeding it to an evaporator under vacuum, having a temperature between 50°C and 85°C.
  • Centrifugation may be carried out with high acceleration rate (more than 2000g) or low acceleration rate (less than 500g) after acidification of the whey protein micelle dispersion at a pH lower than 5, preferably 4.5.
  • Spontaneous sedimentation may also be carried out on the whey protein micelle dispersion by acidification.
  • the pH will be 4.5 and the sedimentation time is more than 12 hours.
  • concentration of the whey protein micelles according to the present invention may be achieved by microfiltration of the micelles dispersion.
  • This enriching technique not only enables to concentrate whey protein micelles by removing the solvent but also enables the removal of non-micellised protein (such as native proteins or soluble aggregates).
  • the final product only consists of micelles (as checked by Transmission Electron Microscopy - cf. figure 9 and 10 ).
  • the concentration factor that is possible to achieve is obtained after the initial flow rate of permeate through the membrane has dropped to 20% of its initial value.
  • the whey protein concentrate obtained by the method of the present invention will have a protein concentration of at least 12%. Furthermore, the concentrate will contain at least 50% of the protein in the form of micelles.
  • the concentrate if adjusted to a protein content of 10% has the ability to withstand a subsequent heat treatment at 85°C for 15 min at pH 7.0 in presence for example of up to 0.15 M of sodium chloride, as shown in Figure 11 .
  • a native whey protein dispersion (Prolacta90, lot 500658 from Lactalis) forms a gel in the presence of 0.1 M of sodium chloride at a protein concentration of only 4% (cf. Figure 12 ).
  • the present invention also presents the benefit that the high stability of the micelle structure is preserved during the concentration step.
  • the micelles have a Protein Efficiency Ratio of at least 100, preferably at least 110, which makes them important nutritional ingredients.
  • the enrichment of the whey protein micelles offers the exceptional advantages that protein-enriched products may be obtained at concentration previously not attainable. Furthermore, since the concentrate may act as a fat substitute while maintaining desirable structural, textural and organoleptic properties, a wider variety of low-fat product may be obtained.
  • the whey protein micelle concentrate (from evaporation or microfiltration) can be used in liquid form as a dispersion or in semi-solid form, or in a dried form. It may be used in a great variety of applications such as those described above with respect to the whey protein micelles applications.
  • the 20% protein concentrate obtained by evaporation has a creamy, semi-solid texture (see Fig. 18 ) and can be texturised in a spreadable texture by acidification using lactic acid.
  • This liquid, creamy, pasty texture can be used to prepare acid, sweet, salty, aromatic, protein-rich consumables.
  • the whey protein micelles concentrate in any form may be mixed with 5% of an acidic fruit base and 5% of sucrose in order to obtain a stable whey protein enriched acidic fruit drink. It may also be used in the manufacture of milk products, ice cream, or used as coffee whitener amongst others.
  • Further applications include skin care and mouth care, such as toothpaste, chewing gum, or gum-cleaning agent for instance.
  • the whitening power of the concentrate in any form is tremendously increased in comparison to the non-concentrated micelles or to the native protein powders.
  • the whitening power of 4mL of a 15% whey protein micelle concentrate is equivalent to 0.3% of titanium oxide in 100mL of a 2% soluble coffee cup.
  • the concentrate may be used as such or diluted depending on the application.
  • the whey protein micelle concentrate in liquid or dried form may be diluted to a protein content of 9% like in sweet and condensed milk.
  • the milk minerals, lactose and sucrose can be added so that the final product will have similar nutritional profile compared to milk, but only whey protein as the protein source.
  • This whey protein based blend is more stable than sweet condensed milk against Maillard reaction (based on the speed of development of a brown colour) when incubated 2 hours at 98°C (temperature of boiling water at an altitude of 833 m).
  • the dried form of the whey protein concentrate obtained by the method of the present invention may be obtained by any known techniques, such as spray-drying, freeze-drying, roller drying etc.
  • the whey protein concentrate may be spray-dried with or without addition of further ingredients and may be used as a delivery system or a building block to be used in a wide range of processes, e.g. consumables production, cosmetic applications etc.
  • Figure 8 shows a powder obtained by spray-drying without addition of any further ingredients, having an average particle diameter size greater than 1 micron due to the micelle aggregation occurring during spray-drying.
  • a typical average volume median diameter (D 43 ) of the powders of the invention is between 45 and 55 microns, preferably 51 microns.
  • the surface median diameter (D 32 ) of the powders is preferably between 3 and 4 microns, more preferably it is 3.8 microns.
  • the moisture content of the powders obtained after spray-drying is preferably less than 10%, more preferably less than 4%.
  • Such a whey protein micelle powder may comprises at least 90% whey protein, from which at least 20%, preferably more than 50%, most preferably more than 80% are in the micellar form.
  • the whey protein micelles powder have a high binding capacity for solvents such as water, glycerol, ethanol, oil, organic solvents etc.
  • the binding capacity of the powders to water is at least 50%, preferably at least 90%, most preferably at least 100%.
  • solvents such as glycerol and ethanol
  • the binding capacity is of at least 50%.
  • oil the binding capacity is at least 30%.
  • This property of the whey protein micelle powders allows these to be sprayed or filled with further functional ingredients such as coffee, caffeine, green tea extracts, plant extracts, vitamins, minerals, bioactive agents, salt, sugar, sweeteners, aroma, fatty acids, oils etc. and mixtures thereof.
  • the functional ingredients may be included in the powder in an amount of 0.1-50%.
  • the powder may act as a carrier for those functional ingredients. This presents the advantage that, for instance, caffeine bitterness perception is reduced when filled into the powders of the present invention and used in caffeinated nutrition bars for instance.
  • Additional ingredients may be mixed to the whey protein micelle concentrate prior to spray-drying. These comprise soluble or non-soluble salts, probiotic bacteria, stains, sugars, maltodextrins, fats, emulsifiers, sweeteners, aroma, plant extracts, ligands, bioactive agents, caffeine, vitamins, minerals, drugs etc. and any possible mixtures thereof.
  • the resulting mixed whey protein micelle powders comprise whey protein micelles and at least one additional ingredient in a weight ratio ranging from 1:1 to 1:1000.
  • Whey protein micelle powders are characterised by a very high flowability, which offers advantages not previously obtainable. For instance, these powders behave almost as liquids and present the advantages of easy usability and transferability.
  • the angle of repose of these powders is preferably below 35°, more preferably below 30°. Such a low angle of repose allows the powders of the present invention to be used as flowing agents in food applications, for instance.
  • FIG. 15 shows a whey protein powder grain which has been sectioned, and whereby the individual whey protein micelles are observable. Furthermore, the micelle structure can be easily reconstituted in solvents. It has been shown that the powders obtained from whey protein micelle concentrate can be easily redispersed in water at room temperature or at 50°C. The size and structure of the whey protein micelles are fully conserved compared to the initial concentrate. For example, in Figure 13 , the whey protein concentrate that was spray-dried at 20% protein concentration has been redispersed in deionised water at 50°C at a protein concentration of 4%.
  • the structure of the micelles has been probed by TEM and can be compared to Figure 10 .
  • a similar shape of micelles was obtained.
  • the diameter of the micelles was found to be 315 nm by dynamic light scattering with a polydispersity index of 0.2.
  • Figure 16 also shows dispersion of a freeze-dried whey protein micelle powder, wherein the micelles are reconstituted.
  • the powders produced according to the process of the present invention may be used in a wide range of applications, such as all those described above in relation to whey protein micelles and the concentrates thereof.
  • protein-enriched consumables such as chocolate, performance nutrition bars, dehydrated culinary products, chewing-gum etc. can be easily produced by using the micelle concentrate powders.
  • the powders produced according to the process of the present invention may also be further coated by emulsifiers or gums, for instance. This may be advantageous to modulate the functionality and the taste of these powders.
  • Example 1 Micellisation of ⁇ -Lactoglobulin by pH adjustment
  • ⁇ -Lactoglobulin (lot JE002-8-922, 13-12-2000) was obtained from Davisco (Le Sueur, MN, USA). The protein was purified from sweet whey by ultra-filtration and ion exchange chromatography. The composition of the powder is 89.7 % protein, 8.85 % moisture, 1.36% ash (0.079 % Ca 2+ , 0.013 % Mg 2+ , 0.097 % K + , 0.576 % Na + , 0.050 % Cl - ). All other reagents used were of analytical grade (Merck Darmstadt, Germany).
  • the protein solution was prepared at 0.2% concentration by solvation of ⁇ -lactoglobulin in MilliQ® water (Millipore), and stirring at 20 °C for 2 h. Then pH of aliquots was adjusted to 5.0, 5.2, 5.4, 5.6, 5.8, 6.0, 6.2, 6.4, 6.6, 6.8, 7.0 by HCl addition.
  • the solutions were filled in 20 ml glass vials (Agilent Technologies) and sealed with aluminum capsules containing a silicon/PTFE sealing. The solutions were heated at 85 °C for 15 min (time to reach the temperature 2.30 - 3.00 min). After the heat treatment, the samples were cooled in ice water to 20 °C.
  • the visual aspect of products ( Figure 1 ) indicates that the optimal pH of micellisation is 5.8.
  • Whey protein isolate (WPI) (Bipro®, Batch JE032-1-420) was obtained from Davisco (Le Sueur, MN, USA). The composition of the powder is reported in table 2.
  • the protein solution was prepared at 3.4% protein by solvation of whey protein powder in MilliQ® water (Millipore), and stirring at 20 °C for 2 h.
  • the initial pH was 7.2.
  • pH of aliquots was adjusted at 5.6, 5.8, 6.0, 6.2, 6.4 and 6.6 by HCl 0.1N addition.
  • the solutions were filled in 20 ml glass vials (Agilent Technologies) and sealed with aluminum capsules containing a silicon/PTFE sealing.
  • the solutions were heated at 85 °C for 15 min (time to reach the temperature 2.30 - 2.50 min). After the heat treatment, samples were cooled in ice water to 20 °C.
  • the turbidity of heated whey proteins has been determined at 500 nm and 25°C, samples were diluted to allow the measurement in the range of 0.1-3 Abs unit (Spectrophotometer Uvikon 810, Kontron Instrument). Values were calculated for the initial protein concentration 3.4%.
  • micellisation The pH of micellisation was considered to be reached upon stability (less than 5% variation of the initial value) of the absorbance measured at 500 nm within an interval of 10 minutes for the same sample as illustrated by the figure 2 .
  • optimal pH for micellisation was 6.0 to 6.2.
  • stable turbidity 21 and residual soluble protein evaluated by absorbance at 280 nm after centrifugation was 1.9%.
  • Table 2 Composition of WPI and sample characteristics after micellisation Supplier Davisco Product name Bipro Batch number JE 032-1-420 Composition (mg/100 g) Sodium 650 Potassium 44 Chloride*10 if ⁇ 40 10 Calcium 82 Phosphorus 49 Magnesium 6 Initial pH 7.2 pH micellisation 6.0 Turbidity (500 nm)for 3.4% protein in solution 21 Residual Soluble protein (%) by absorbance at 280 nm 1.9
  • Protein solution was prepared at 2% protein by solvation of whey protein powder (WPI 90 batch 989/2, Lactalis, Retier, France) in MilliQ® water (Millipore), and stirred at 20 °C for 2 h. Then pHs of aliquots were adjusted using HCl 0.1N or NaOH 0.1N.
  • micellisation The solutions were filled in 20 ml glass vials (Agilent Technologies) and sealed with aluminum capsules containing a silicon/PTFE sealing. The solutions were heated at 85°C for 15 min (time to reach the temperature 2.30-2.50 min). After the heat treatment, the samples were cooled in ice water to 20 °C. For this product the optimal pH for micellisation was 7.4.
  • Liquid micelle samples were encapsulated in agar gel tubes. Fixation was achieved by immersion in a solution of 2.5% glutaraldehyde in 0.1M, pH 7.4 cacodylate buffer and post-fixation with 2% Osmium tetroxide in the same buffer, both solutions containing 0.04% Ruthenium red. After dehydration in a graded ethanol series (70, 80, 90, 96, 100% ethanol), the samples were embedded in Spurr resin (Spurr/ethanol 1:1, 2:1, 100%). After polymerization of the resin (70°C, 48 hours), semi-thin and ultra-thin sections were cut with a Leica ultracut UCT ultra-microtome. Ultra-thin sections, stained with aqueous uranyl-acetate and lead citrate, were examined in transmission electron microscopy (Philips CM12, 80 kV).
  • TEM micrograph is presented in figure 3 .
  • Obtained micelles are presenting a spherical shape with a diameter of 200 nm.
  • the intensity-based size distributions of micelles were measured for those micelles obtained by heat-treatment of a 1 wt % ⁇ -lactoglobulin dispersion for 15 min at 85°C at pH 4.25 (positively charged with a zeta potential around +25mV) and at pH 6.0 (negatively charged with a zeta potential around -30mV).
  • Z-averaged hydrodynamic diaemeter of the micelles was 229.3 mm at pH 4.25 an 227.2 at pH 6.0.
  • ⁇ -LG and whey protein aggregations were followed using dynamic light scattering.
  • a Nanosizer ZS apparatus (Malvern Instruments, UK) equipped with a laser emitting at 633 nm and with 4.0 mW power was used.
  • the instrument was used in the backscattering configuration, where detection is done at a scattering angle of 173°. This allows considerable reduction of the multiple scattering signals found in turbid samples.
  • Samples were placed in a squared quartz cell (Hellma, pathlength 1 cm). The path length of the light beam was automatically set by the apparatus, depending on the sample turbidity (attenuation). The autocorrelation function was calculated from the fluctuation of the scattered intensity). The results are presented in figure 6 . It shows that the average particle is characterized by a very narrow polydispersity index ( ⁇ 0.200). In consequence, the white suspension obtained by the present invention is stable and has a milky appearance in a large range of pH 3-8.
  • Example 4 Micellisation of a ⁇ -lactoglobulin at a constant pH (Reference)
  • Example 1 The method described in example 1 was repeated using an aqueous solution of 2% ⁇ -lactoglobulin.
  • the pH of this solution has been adjusted to 7.0 after adding Arginine HCl solutions to obtain a final salt concentration ranging from 5 to 200 mM and a final ⁇ -lactoglobulin concentration of 1%.
  • Subsequent heat treatment 80 °C, 10 min, about 2 min heating up was carried out to produce micelles.
  • Example 7 Preparing an aqueous foam (Reference)
  • Native ⁇ -lactoglobulin (Biopure, Davisco, lot JE 002-8-922, 2 wt-% aqueous solution) was mixed with 120 mM Arginine HCl solution so that the final ⁇ -lactoglobulin concentration was 1 wt.% and Arginine HCl 60 mM. The pH was then adjusted to 7.0 by addition of 1N HCl. The mixture was then heat treated at 80°C for 10 minutes so that 90% of initial ⁇ -lactoglobulin was converted into micelles having a z-averaged diameter of 130 nm. In this case, the diameter of the micelles was determined using a Nanosizer ZS apparatus (Malvern Instruments, UK).
  • the sample was poured in a quartz cuvette and variations of the scattered light were recorded automatically.
  • the obtained autocorrelation function was fitted using the cumulants method so that the diffusion coefficient of the particles could be calculated and thereafter the z-averaged hydrodynamic diameter using the Stokes-Einstein law.
  • the refractive index of the solvent was taken as 1.33 and that of the micelles 1.45.
  • a volume of 50 mL of the resulting dispersion of ⁇ -lactoglobulin micelles is then foamed by nitrogen sparging through a glass frit generating bubbles of 12-16 ⁇ m to produce a foam volume of 180 cm 3 using the standardised Foamscan TM (ITConcept) apparatus.
  • Fig. 5 shows that the foam volume stability is greatly improved by the presence of ⁇ -lactoglobulin micelles.
  • Example 8 Whey based Fermented dairy product - fermentation trials
  • Whey protein isolate (WPI) (Bipro®) was obtained from Davisco (Le Sueur, MN, USA) (protein concentration 92.7%).
  • Spray dried whey permeate (Variolac 836): Lactose concentration: 83 % -Minerals: 8% Lactic Acid 50 % Edible Lactose (Lactalis) De-ionized water
  • the Bipro® powder was dissolved in de-ionized water in order to have a protein concentration of 4.6 %, i.e. for 3 litres of solution 154.5 g of WPI powder and 2845.5 g of water.
  • the hydration time was 3 hours. After hydration, this solution has been divided in samples of 200 ml to prepare the different trials: Table 3 Trial Whey permeate (%) Lactose (%) pH adjustment Heating 85°C / 15 min 1 2.9 2.5 6.5 + 2 0 5 6 + 3 0 5 6.7 - 4 0 5 6.7 + 5 0 5 6.1 + 6 0 0 6 + 7 0 5 (added after pH adjustment) 6 - 8 0 5 (added after pH adjustment) 6 +
  • lactic acid at 50 % has been added to adjust the pH before heating.
  • Samples were heated with the double boiler up to 85°C and maintain at this temperature during 15 minutes. After heating, solutions were cooled at 40°C and inoculated with Lactobacillus bulgaricus and Streptococcus thermophilus.
  • Samples were incubated 5h30 in a steam room at 41°C before to be placed in a cold room at 6°C.
  • Example 9 Whey protein boosted ice cream with reduced fat content
  • Whey protein isolate (WPI, Prolacta90® from Lactalis, Rétiers, France) with a protein content of 90% Skim milk powder with 35% protein content Sucrose Maltodextrins DE39 Anhydrous milk fat Emulsifier De-ionised water Edible hydrochloric acid 1M
  • the Prolacta90® powder was dispersed at 50°C in de-ionized water at a protein concentration of 9.67 wt% under gentle stirring in order to avoid foam formation, i.e. 3.3 kg of Prolacta90® were dispersed in 31.05 kg of de-ionised water.
  • the pH of the dispersion was adjusted to the micellisation pH by addition of HCl.
  • the temperature of the dispersion was raised to 85°C and maintained for 15 minutes in order to generate the whey protein micelles. After 15 minutes, the temperature was decreased to 50°C and the additional ingredients were sequentially added to the micelles dispersion (i.e.
  • skim milk powder maltodextrins DE39, sucrose, emulsifier and anhydrous milk fat.
  • the final amount of mix was 50 kg with total solids content of 39.5% and a fat content of 5 wt%. After 30 minutes of hydration, the mix was two-step homogenised (80/20 bars) and pasteurised (86°C/30s) before ageing during overnight.
  • the final ice cream contained 8wt% proteins (20% caseins, 80% whey proteins) and 5 wt% fat on the ice cream mix basis.
  • Example 10 Powdered whey protein micelles obtained by spray-drying
  • Whey protein isolate (WPI, Prolacta90® from Lactalis, Rétiers, France) with a protein content of 90% Edible lactose Maltodextrins DE39 De-ionised water Edible hydrochloric acid 1M
  • the Prolacta90® powder was dispersed at 50°C in de-ionized water at a protein concentration of 10 wt% under gentle stirring in order to avoid foam formation, i.e. 11 kg of Prolacta90® were dispersed in 89 kg of de-ionised water.
  • the pH of the dispersion was adjusted to the micellisation pH (around 6.3 in that case) by addition of HCl.
  • the temperature of the dispersion was raised to 85°C and maintained for 15 minutes in order to generate the whey protein micelles. After 15 minutes, the temperature was decreased to 50°C and the 10 wt% whey protein micelles dispersion was split in two batches of 50 kg.
  • the two mixtures were then spray dried into a NIRO SD6.3N tower at a flow rate of 15 L/h.
  • the air input temperature was 140°C and the air output temperature was 80°C.
  • the water content of the obtained powders was lower than 5%.
  • the size of the whey protein micelles was determined in presence of lactose and maltodextrin (DE39) in water using dynamic light scattering before and after spray drying.
  • the total protein concentration was set to 0.4 wt% by dilution of the dispersion before spray drying or reconstitution of the powder in order to be in the dilute regime of viscosity for whey protein micelles.
  • a Nanosizer ZS apparatus (Malvern Instruments) was used and micelle diameter was averaged from 20 measurements.
  • the particle diameter determined for whey protein micelles in presence of lactose and maltodextrins (DE39) was 310.4 nm and 306.6, respectively. After reconstitution of the powders, the respective diameters were found to be 265.3 nm and 268.5, respectively. These measurements confirm than whey protein micelles were physically stable regarding spray drying. The results were corroborated by TEM microscopy observations of 0.1 wt% whey protein micelles dispersions in water using negative staining in presence of 1% phosphotungstic acid at pH 7. A Philips CM12 transmission electron microscope operating at 80 kV was used. Whey protein micelles were observed in solution before spray drying and after reconstitution of the spray-dried powder. No difference of morphology and structure could be detected.
  • a whey protein isolate Prolacta 90 from Lactalis (lot 500648) has been reconstituted at 15°C in soft water at a protein concentration of 4% to reach a final batch size of 2500 kg.
  • the pH was adjusted by addition of 1M hydrochloric acid so that the final pH value was 5.90.
  • the whey protein dispersion was pumped through plate-plate APV-mix heat exchanger at a flow rate of 500 l/h. Pre-heating at 60°C was followed by heat treatment of 85°C for 15 minutes. Formation of whey protein micelles was checked by measurement of particle size using dynamic light scattering as well a turbidity measurement at 500 nm.
  • the obtained 4% whey protein micelles dispersion was characterised by a hydrodynamic radius of particles of 250 nm, a polydispersity index of 0.13 and a turbidity of 80.
  • the whey protein micelle dispersion was then used to feed a Scheffers evaporator at a flow rate of 500 1/h.
  • the temperature and vacuum in the evaporator were adapted so that around 500 kg whey protein micelles concentrate having a protein concentration 20% were produced and cooled down to 4°C.
  • a whey protein isolate Prolacta 90 from Lactalis (lo 500648) has been reconstituted at 15°C in soft water at a protein concentration of 4% to reach a final batch size of 2500 kg.
  • the pH was adjusted by addition of 1M hydrochloric acid so that the final pH value was 5.90.
  • the whey protein dispersion was pumped through plate-plate APV-mix heat exchanger at a flow rate of 500 L/h.
  • a pre-heating at 60°C was followed by heat treatment of 85°C for 15 minutes. Formation of whey protein micelles was checked by measurement of particle size using dynamic light scattering as well a turbidity measurement at 500 nm.
  • the obtained 4% whey protein micelles dispersion was characterised by a hydrodynamic radius of particles of 260 nm, a polydispersity index of 0.07 and a turbidity of 80.
  • the micelle form of the protein was also checked by TEM, and micelle structures with an average diameter of 150-200 nm were clearly visible ( Fig. 9 ).
  • the whey protein micelle dispersion was cooled at 4°C and used to feed a filtration unit equipped with a 6.8 m 2 Carbosep M14 membrane at a flow rate of 180 L/h. In that case, the concentration of the whey protein micelles was performed at 10°C until the permeate flow rate reached 70 L/h. In that case, the final whey protein concentrate contained 20% of proteins.
  • the structure of the micelles in the concentrate was checked by TEM, and clearly no significant change was visible compared to the 4% whey protein dispersion before microfiltration ( Fig. 10 ).
  • Example 13 Whey protein micelles powder comprising at least 90% whey protein
  • Example 14 Mixed whey protein micelle powder
  • the powders of examples 13 and 14, when reconstituted in water, comprise essentially micelles having the same structure and morphology as the whey protein micelle concentrate.
  • Example 15 Whey protein micelle powder obtained by freeze-drying
  • Whey protein micelle concentrate at 20% protein produced by microfiltration in example 12 with a protein content of 90%
  • whey protein micelles concentrate 100g were introduced in a plastic beaker and frozen at -25°C for one week. This beaker was then placed in a lab-scale freeze drier Virtis equipped with a vacuum pump. Sample was left for 7 days until the pressure in the freeze drier remained constant at about 30 mbars. Around 20 g of freeze-dried whey protein micelles has been recovered.
  • Example 16 A whey protein enriched dark chocolate without sucrose
  • Cocoa liquor is mixed with cocoa butter, butter fat, whey protein micelle powder, sucralose, vanillin and lecithin. This mixture is conched overnight at 65°C until a homogenous paste is obtained. This chocolate mass is then moulded in chocolate plates and cooled down. The dark chocolate is characterized by a final whey protein content of 45-50%.
  • Example 17 A whey protein enriched white chocolate
  • Method 1 Method 2
  • Method 3 Whey protein micelle powder from example 13 with a protein content of 90% 15-25% 25-35% 35-40% Sucrose 40-45% 30-35% 30-35%
  • Anhydrous milk fat 1-10% 1-10% 1-10% Whey powder 2-10% 2-10% 0% Cocoa butter 20-30% 20-30% 20-30% Vanillin 0.01-0.1% 0.01-0.1% 0.01-0.1%
  • Lecithin 0.1-1% 0.1-1% 0.1-1% 0.1-1% 0.1-1% 0.1-1% 0.1-1% 0.1-1% 0.1-1% 0.1-1% 0.1-1%
  • Whey protein micelles, whey powder, sucrose and vanillin are mixed and ground until the desired particle size distribution is obtained. This mixture is then conched overnight at 65°C with cocoa butter, anhydrous milk fat and lecithin until a homogenous paste is obtained. This chocolate mass is then moulded in chocolate plates and cooled down. This white chocolate is characterized by a final whey protein content of 20%.
  • Whey protein micelles, whey powder, sucrose and vanillin are mixed and ground until the desired particle size distribution is obtained. This mixture is then conched overnight at 65°C with cocoa butter, anhydrous milk fat and lecithin until a homogenous paste is obtained. This chocolate mass is then moulded in chocolate plates and cooled down. This white chocolate is characterized by a final whey protein content of 30%.
  • Whey protein micelles, sucrose and vanillin are mixed and ground until the desired particle size distribution is obtained. This mixture is then conched overnight at 65°C with cocoa butter, anhydrous milk fat and lecithin until a homogenous paste is obtained. This chocolate mass is then moulded in chocolate plates and cooled down. This white chocolate is characterized by a final whey protein content of 30-35%.
  • Example 18 Aqueous dispersion of whey protein micelles coated with sulfated butyl oleate (SBO) or any other negatively charged emulsifier
  • WPM powder described in example 13 is dispersed in MilliQ water to achieve a final protein concentration of 0.1 wt%. This dispersion is filtered on 0.45 ⁇ m filters in order to remove possible WPM aggregates. The pH of this WPM dispersion was brought down to 3.0 by addition of hydrochloric acid 1M. A 1 wt% dispersion of SBO is prepared at pH 3.0.
  • the hydrodynamic radius and zeta potential of these WPM was determined using the Nanosizer ZS apparatus (Malvern Instruments Ltd.). Diameter was 250 nm and electrophoretic mobility + 2.5 ⁇ m.cm.V -1 .s -1 .
  • the hydrodynamic radius and electrophoretic mobility of the SBO dispersion at pH 3.0 are 4 nm and - 1.5/-2.0 ⁇ m.cm.V -1 .s -1 , respectively.
  • the SBO dispersion is used to titrate the WPM one, while following evolution of hydrodynamic radius and electrophoretic mobility of the mixture. It was found that the hydrodynamic radius was constant around 250-300 nm until a WPM/SBO weight-mixing ratio of 5:1 was reached. At this point, the hydrodynamic radius diverges dramatically to 20000 nm and precipitation of complexes WPM SBO is encountered. Upon further addition of SBO, higher than a mixing ratio of 5:1, the hydrodynamic progressively decreased to 250 nm, as found initially for WPM, levelling of from a ratio of 4:1 on. Following the electrophoretic mobility of the mixture showed that it decreased upon addition of SBO, reaching zero value for a mixing ratio of 5:1. Then it continued to drop upon SBO addition, starting levelling of at - 3.0 ⁇ m.cm.V -1 .s -1 from ratio 4:1 on.
  • Emulsifiers such as DATEM, CITREM, SSL (from Danisco) in aqueous solution at pH 4.2 where they are mainly ionized in their anionic form (-COO - chemical functions).
  • Example 19 A protein-enriched bechamel sauce
  • Example 20 A whey protein-enriched base for performance bar
  • Brown rice syrup is mixed with maltitol and glycerol at 25°C.
  • Whey protein micelle powder is then added and mixing is performed for 10 minutes.
  • a whey protein-enriched base for performance bar is then obtained and can be mixed with other ingredients (minerals, vitamins, flavours). This preparation contains more proteins than milk (38%).
  • Example 21 Determination of repose angle for spray dried whey protein micelle powder, mixed whey protein micelle powder, whey protein isolate powder and low heat skim milk powder
  • Whey protein isolate powder Prolacta 90 (lot 500658 from Lactalis, France; moisture 4%)
  • Low heat skim milk powder (lot 334314 from Emmi, Switzerland; moisture 3.5%) Measuring device described to measure repose angle for powders according to ISO norm 4324
  • the powder is placed in a funnel with a stem diameter of 99 mm and the powder is forced to flow using the agitator.
  • the powder falls on a transparent plastic vessel with diameter 100 mm and a height of 25 mm.

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Claims (14)

  1. Procédé pour la production de concentré de micelles de protéine de lactosérum étant constitué des étapes suivantes :
    a. ajuster le pH d'une solution aqueuse déminéralisée de protéine de lactosérum à un pH entre 5,8 et 6,6, la concentration de la solution aqueuse de protéine de lactosérum étant inférieure à 12 % et, si la solution aqueuse de protéine de lactosérum comprend des composés additionnels, la quantité desdits composés additionnels n'excédant pas 10 % en poids du poids total de la solution,
    b. soumettre la solution aqueuse à une température entre 80 et 89 °C, le chauffage étant réalisé pendant une période de temps allant de 10s à 2 heures.
    c. concentrer la dispersion obtenue dans l'étape b et
    d. optionnellement, sécher par pulvérisation et lyophiliser le concentré de micelles de protéine de lactosérum.
  2. Procédé selon la revendication 1, dans lequel la concentration de solution aqueuse de protéine de lactosérum est inférieure à 4 %.
  3. Procédé selon la revendication 1, dans lequel le temps de chauffage est de 15 minutes.
  4. Procédé selon l'une des revendications précédentes, dans lequel le chauffage est réalisé par micro-ondes.
  5. Procédé selon l'une des revendications précédentes, dans lequel le rendement en micelles avant la concentration est d'au moins 35 %.
  6. Procédé selon la revendication 5, dans lequel le rendement en micelles avant la concentration est d'au moins 50 %.
  7. Procédé selon les revendications 5 et 6, dans lequel le rendement en micelles avant la concentration est d'au moins 80 %.
  8. Procédé selon l'une des revendications précédentes, dans lequel les micelles ont une taille moyenne de moins de 1 micron.
  9. Procédé selon la revendication 8, dans lequel les micelles ont une taille moyenne de 100-900 nm, de préférence 100-700 nm, encore plus préférablement 200-400 nm.
  10. Procédé selon l'une des revendications précédentes, dans lequel la proportion de micelles avec une taille moyenne comprise entre 100 nm et 700 nm est supérieure à 80%.
  11. Procédé selon l'une des revendications précédentes, dans lequel la concentration est réalisée par évaporation, centrifugation, sédimentation ou microfiltration.
  12. Procédé selon la revendication 11, dans lequel la centrifugation est réalisée à taux d'accélération haut ou bas après acidification au pH de 4,5.
  13. Procédé selon la revendication 11, dans lequel une sédimentation spontanée est réalisée au pH de 4,5.
  14. Procédé selon la revendication 13, dans lequel le temps de sédimentation est supérieur à 12 heures.
EP06006295A 2004-09-29 2006-03-27 Micelles de lactosérum Not-in-force EP1839492B1 (fr)

Priority Applications (27)

Application Number Priority Date Filing Date Title
EP06006295A EP1839492B1 (fr) 2006-03-27 2006-03-27 Micelles de lactosérum
AT06006295T ATE524073T1 (de) 2006-03-27 2006-03-27 Molkenprotein micellen
ES06006295T ES2373400T3 (es) 2006-03-27 2006-03-27 Micelas de proteína láctea.
PL06006295T PL1839492T3 (pl) 2006-03-27 2006-03-27 Micele białka serwatkowego
MYPI20070461A MY161874A (en) 2006-03-27 2007-03-23 Whey protein micelles
AU2007231336A AU2007231336B2 (en) 2004-09-29 2007-03-26 Whey protein micelles
RU2008142397/10A RU2417622C2 (ru) 2006-03-27 2007-03-26 Мицеллы белка молочной сыворотки
CA2643651A CA2643651C (fr) 2006-03-27 2007-03-26 Micelles de proteines de lactoserum
NZ571141A NZ571141A (en) 2006-03-27 2007-03-26 Whey protein micelles
PCT/EP2007/052877 WO2007110411A2 (fr) 2006-03-27 2007-03-26 Micelles de proteines de lactoserum
EP07727350A EP2001306A2 (fr) 2006-03-27 2007-03-26 Micelles de proteines de lactoserum
CN2007800113474A CN101410025B (zh) 2006-03-27 2007-03-26 乳清蛋白微胶粒
UAA200812529A UA98934C2 (uk) 2006-03-27 2007-03-26 Міцели білка молочної сироватки
CN2007800110423A CN101410020B (zh) 2006-03-27 2007-03-27 乳清蛋白微胶粒
US12/280,244 US8399043B2 (en) 2006-03-27 2007-03-27 Whey protein micelles
AU2007231346A AU2007231346A1 (en) 2006-03-27 2007-03-27 Whey protein micelles
PCT/EP2007/052900 WO2007110421A2 (fr) 2006-03-27 2007-03-27 Micelles de protéines de lactosérum
RU2008142396/13A RU2008142396A (ru) 2006-03-27 2007-03-27 Мицеллы сывороточного протеина
UAA200812429A UA98763C2 (ru) 2006-03-27 2007-03-27 Концентрат мицелл сывороточного протеина и способ его получения
EP07727373A EP1998626A2 (fr) 2006-03-27 2007-03-27 Micelles de lactosérum
ARP070101277A AR060163A1 (es) 2006-03-27 2007-03-27 Micelas de proteina de suero
CA2640684A CA2640684C (fr) 2006-03-27 2007-03-27 Micelles de proteines de lactoserum
JP2009502066A JP2009531043A (ja) 2006-03-27 2007-03-27 乳清タンパク質ミセル
MX2008012184A MX2008012184A (es) 2006-03-27 2007-03-27 Micelas de proteina de suero.
IL193863A IL193863A (en) 2006-03-27 2008-09-02 An edible product containing milk protein and a method for making it
ZA2008/09154A ZA200809154B (en) 2006-03-27 2008-10-24 Whey protein micelles
US13/780,975 US20130171318A1 (en) 2006-03-27 2013-02-28 Whey protein micelles

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Application Number Priority Date Filing Date Title
EP06006295A EP1839492B1 (fr) 2006-03-27 2006-03-27 Micelles de lactosérum

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EP1839492B1 true EP1839492B1 (fr) 2011-09-14

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EP06006295A Not-in-force EP1839492B1 (fr) 2004-09-29 2006-03-27 Micelles de lactosérum
EP07727350A Withdrawn EP2001306A2 (fr) 2006-03-27 2007-03-26 Micelles de proteines de lactoserum
EP07727373A Withdrawn EP1998626A2 (fr) 2006-03-27 2007-03-27 Micelles de lactosérum

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EP07727350A Withdrawn EP2001306A2 (fr) 2006-03-27 2007-03-26 Micelles de proteines de lactoserum
EP07727373A Withdrawn EP1998626A2 (fr) 2006-03-27 2007-03-27 Micelles de lactosérum

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EP (3) EP1839492B1 (fr)
JP (1) JP2009531043A (fr)
CN (2) CN101410025B (fr)
AR (1) AR060163A1 (fr)
AT (1) ATE524073T1 (fr)
AU (2) AU2007231336B2 (fr)
CA (2) CA2643651C (fr)
ES (1) ES2373400T3 (fr)
IL (1) IL193863A (fr)
MX (1) MX2008012184A (fr)
MY (1) MY161874A (fr)
NZ (1) NZ571141A (fr)
PL (1) PL1839492T3 (fr)
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AU2007231346A1 (en) 2007-10-04
JP2009531043A (ja) 2009-09-03
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UA98934C2 (uk) 2012-07-10
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US8399043B2 (en) 2013-03-19
UA98763C2 (ru) 2012-06-25
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US20130171318A1 (en) 2013-07-04
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US20090035437A1 (en) 2009-02-05
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CA2640684C (fr) 2015-02-03
CN101410025A (zh) 2009-04-15
WO2007110411A3 (fr) 2008-07-10
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PL1839492T3 (pl) 2012-02-29
AR060163A1 (es) 2008-05-28
EP1839492A1 (fr) 2007-10-03
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IL193863A (en) 2014-11-30
MY161874A (en) 2017-05-15

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